The present invention relates to a spray nozzle for a two-component, air-assisted, low pressure spray system including
1) a static mixer having an upstream end and a downstream end wherein
a) the upstream end has an inlet port for receiving a first liquid component and a second liquid component that is reactive with the first liquid component and the upstream end is dimensioned to be reversibly connected to a dispensing unit for the first and second liquid components, and
b) the downstream end has an optionally removable spray tip for introducing the mixed liquid components into an atomizing zone and the downstream end is dimensioned for reversibly connecting the static mixer to a spray section, and
2) a spray section having an upstream end and a downstream end wherein
a) the upstream end of the spray section is dimensioned for being reversibly connecting to the static mixer,
b) the spray section has inlet ports for receiving pressurized air and
c) the downstream end of the spray section has outlet ports for introducing air into an atomizing zone formed between the outlet ports and the spray tip,
wherein the spray tip of the static mixer passes through an orifice in the spray section such that the mixed liquid components are introduced into the atomizing zone.
|
10. A process for spraying a two-component composition which comprises
a) introducing a first liquid component and a second liquid component, which is reactive with the first liquid component, into a static mixer having an optionally removable spray tip, b) mixing the first component with the second component in the static mixer, c) discharging the mixed liquid components from the static mixer through the optionally removable spray tip at the downstream end of the static mixer into an atomizing zone, d) introducing air into the atomizing zone, e) atomizing the mixed liquid components in the atomizing zone, f) spraying the atomized liquid components onto a substrate and g) during an interruption in the spraying process or after termination of the spraying process, discarding the static mixer and the optionally removable spray tip.
1. A spray nozzle for a two-component, air-assisted, low pressure spray system comprising
1) a static mixer having an upstream end and a downstream end wherein a) the upstream end has an inlet port for receiving a first liquid component and a second liquid component that is reactive with the first liquid component and the upstream end is dimensioned to be connected and unconnected to a dispensing unit for the first and second liquid components, and b) the downstream end has an optionally removable spray tip for introducing the mixed liquid components into an atomizing zone and the downstream end is dimensioned for connecting and unconnecting the static mixer to a spray section, and 2) a spray section having an upstream end and a downstream end wherein a) the upstream end of the spray section is dimensioned for being connecting and unconnecting to the static mixer, b) the spray section has inlet ports for receiving pressurized air and c) the downstream end of the spray section has outlet ports for introducing air into an atomizing zone formed between the outlet ports and the spray tip, wherein the spray tip of the static mixer passes through an orifice in the spray section such that the mixed liquid components are introduced into the atomizing zone.
4. The spray nozzle of
5. The spray nozzle of
7. The spray nozzle of
8. The spray nozzle of
11. The process of
|
1. Field of the Invention
The present invention relates to an improved spray nozzle for a two-component, air-assisted, low pressure spray system, which is especially suited for applying highly reactive, two-component coating or sealing compositions, preferably two-component polyurea coating compositions.
2. Description of the Prior Art
Several types of spray systems are known for applying two-component coating compositions. If the two components are not highly reactive, it is possible to mix the two components prior to use and apply the systems with known one-component, airless or air-assisted spray systems. These systems are generally used with coating compositions having a pot life of one hour to several hours.
Preferably, the two-component compositions are applied with two-component spray systems, which may be either high pressure (more than 100 bar) or low pressure (less than 100 bar) systems. The high pressure systems are usually airless or air-assisted airless spray systems. In these systems the two components are generally introduced under high pressure into a static mixer and are then passed through a spray tip under sufficient pressure to atomize the liquid. One disadvantage of these systems is their high cost.
Also suitable are low pressure or high pressure impingement mixers in which the components are introduced through separate orifices into a mixing chamber and then pass through an atomization spray tip under fluid pressure. The mixing chamber is generally purged with a purge rod or pressurized air. Disadvantages of impingement mixing systems are their cost, difficulty to use and typical high pressure requirements.
Examples of low pressure systems for applying two-component compositions are air-assisted sprayers in which the components are premixed and then siphoned or passed by gravity through an air atomization tip. Air is passed in a generally perpendicular manner to the mixed composition from opposing outlets to atomize the composition into the desired spray pattern. A disadvantage of these spray systems is that they are not suitable for spraying highly reactive two-component systems. Both during the spraying process and especially during stoppages, the components can react to form polymer solids that clog both the liquid spray tips and/or the air outlets. This causes a lengthy down time to clean the equipment for further use.
One alternative to prevent clogging in any of these low or high pressure sprayers is to flush the equipment with a solvent or an air purge prior to stoppages. However, this embodiment results in higher equipment costs due to the presence of a third stream. In addition, the use of a solvent is disadvantageous both from a cost standpoint and an environmental standpoint.
It is an object of the present invention to overcome the disadvantages of prior art spray systems in a cost effective manner.
This object may be achieved with the low pressure, two-component, air-assisted spray system according to the present invention. An important feature of the invention is the use of a disposable static mixer having an optionally removable spray tip to eliminate the clogging problems of prior art systems when spraying highly reactive two-component systems.
Copending application, U.S. Ser. No. 09/838,794, describes a static mixer having an optionally removable spray tip, but in that application the static mixer is inserted into a shroud. U.S. Ser. Nos. 09/917,309 and 09/917,298 also describe static mixers having optionally removable spray tips, but these applications require the static mixers to be used in combination with caulking guns.
The present invention relates to a spray nozzle for a two-component, air-assisted, low pressure spray system including
1) a static mixer having an upstream end and a downstream end wherein
a) the upstream end has an inlet port for receiving a first liquid component and a second liquid component that is reactive with the first liquid component and the upstream end is dimensioned to be reversibly connected to a dispensing unit for the first and second liquid components, and
b) the downstream end has an optionally removable spray tip for introducing the mixed liquid components into an atomizing zone and the downstream end is dimensioned for reversibly connecting the static mixer to a spray section, and
2) a spray section having an upstream end and a downstream end wherein
a) the upstream end of the spray section is dimensioned for being reversibly connecting to the static mixer,
b) the spray section has inlet ports for receiving pressurized air and
c) the downstream end of the spray section has outlet ports for introducing air into an atomizing zone formed between the outlet ports and the spray tip,
wherein the spray tip of the static mixer passes through an orifice in the spray section such that the mixed liquid components are introduced into the atomizing zone.
The present invention also relates to a process for spraying a two-component composition by
a) introducing a first liquid component and a second inlet component, which is reactive with the first liquid component, into a static mixer having an optionally removable spray tip,
b) mixing the first component with the second component in the static mixer,
c) discharging the mixed liquid components from the static mixer through the optionally removable spray tip at the downstream end of the static mixer into an atomizing zone,
d) introducing air into the atomizing zone,
e) atomizing the mixed liquid components in the atomizing zone,
f) spraying the atomized liquid components onto a substrate and
g) during an interruption in the spraying process or after termination of the spraying process, discarding the static mixer and the optionally removable spray tip.
In accordance with the present invention it is possible to overcome the problem of clogging in the static mixer, the spray tip and/or air entry ports when spraying highly reactive, two-component compositions. This is accomplished by using a removable static mixer having an optionally removable spray tip at the downstream end. In one embodiment the static mixer tapers at the downstream end to form a spray tip. In a preferred embodiment a removable spray tip is attached to the downstream end of the static mixer. In accordance with this preferred embodiment different size spray tips can be attached to control the volume of material to be sprayed.
The static mixers can be made of metal or plastic or other suitable materials. They are preferably made from plastic for cost reasons because at the completion of the spraying process or during periods when the spraying process is interrupted, the static mixer and the optionally removable spray tip are removed and discarded. However, the pressure limitations of the static mixers should not be exceeded. Accordingly, when operating at higher pressures, it may be necessary to use metal or other specially designed static mixers that can withstand the operating pressure.
Examples of suitable static mixers are available as motionless mixers from Tah Industries. Examples include stainless tube mixers, stainless pipe mixers, stainless/plastic pipe mixers and plastic tube mixers. Removable spray tips are also available from Tah Industries as Luer lock fitting needles.
In accordance with the present invention the upstream end of the static mixer is dimensioned to be reversibly connected to a dispensing unit for the first and second liquid components and the downsteam end of the static mixer is dimensioned to be reversibly connected to the spray section. The type of connection is not critical, provided that the connection is reversible so that the static mixer and the optionally removable spray tip can be discarded. Suitable connections include threads, clamps, retaining rings and quick connectors.
In one embodiment, which is shown in
The upstream end of a conventional spray section having an atomizing zone is connected to the downstream end of the static mixer. Both ends are dimensioned to be reversibly connected to each other. This connection can be the same as those set forth previously for connecting the upstream end of the static mixer to the dispensing unit. The spray tip extends through an orifice in the rear portion of the spray section and into the atomizing zone.
After the components are mixed in the static mixer they are introduced into the atomizing zone of the spray section where the mixed components are atomized with air, which may compressed in known manner in a compressor. Methods of atomizing the liquid components with air for spraying are well known and are not critical to the present invention. In a preferred embodiment as shown in
Air may also be introduced through the same orifice in the spray section that the spray tip passes through. In this embodiment the air passes on the outside of the spray tip parallel to the mixed components. However, less atomization occurs according to this embodiment. It is also possible to introduce air at other angles to the liquid components that range from parallel to perpendicular or slightly greater.
The method of introducing reactive first and second components into the static mixer is not critical and does not form a part of the spray nozzle according to the present invention. Any apparatus that is known for accurately metering plural components is suitable for use as the delivery means. Suitable apparatus is available from Adhesive Systems Technology (AST) Corporation as metering and dispensing equipment for plural component reactive systems. The upstream end of the shroud is dimensioned to be reversibly connected to the plural component dispensing unit of the metering and dispensing equipment.
In accordance with the process of the present invention the first and second liquid components are preferably introduced into the static mixer at a pressure of 5 to 100 bar, more preferably 10 to 100 and most preferably 30 to 70 bar, which is supplied by the dispensing equipment. The components are then mixed in the static mixer and discharged through the optionally removable spray tip at the downstream end of the static mixer into an atomizing zone. Air is also introduced into the atomizing zone at a pressure of preferably 0.5 to 10 bar, preferably 1 to 7 bar and more preferably 3 to 6 bar. The atomized liquid components are then applied to a suitable substrate.
Suitable first and second components include any compounds that are reactive with each other to form a polymer. Examples include the reaction of polyisocyanates with polyols to form polyurethanes, the reaction of polyisocyanates with polyamines to form polyureas and the reaction of epoxy resins or epoxidized urethanes with amine curatives to form polyamides. Examples of suitable components are well known. Preferred components are those that are highly reactive with each other, e.g. those that cure or react with each other within a few minutes to a few seconds. When spraying these types of components any interruption of the spraying operation results in clogging of the static mixer, especially the spray tip and occasionally the air inlets to the atomizing zone.
An example of highly reactive components are the polyisocyanates and polyaspartates described in U.S. Pat. Nos. 5,126,170 and 5,236,741, which are herein incorporated by reference.
Static mixer 1 and spray tip 5 are inserted through spray section 10 such that end 6 extends into atomizing zone 16. Static mixer 1 has threaded end 7 for attaching to a dispensing unit for the two-component composition and threaded end 8 for connecting to spray section 10. Air is introduced into atomizing zone 16 via tube 12 through outlet ports in modified fluid nozzle 15 and through outlet ports 9 in air cap 14. Air cap 14 is held against the modified fluid nozzle 15 by attaching threaded retaining ring 17 to threads 13 of spray section 10. In atomizing zone 16, the air passing through outlet ports 9 atomizes the liquid stream of the two-component coating composition passing through static mixer 1 and end 6 of spray tip 5.
Although the invention has been described in detail in the foregoing for the purpose of illustration, it is to be understood that such detail is solely for that purpose and that variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention except as it may be limited by the claims.
Patent | Priority | Assignee | Title |
10434538, | Jul 19 2017 | 4 C's Spray Equipment Rental, LLC | Adhesive dispensing system and method |
10751748, | Jul 19 2017 | 4 C's Spray Equipment Rental, LLC; 4 C S SPRAY EQUIPMENT RENTAL, LLC | Adhesive dispensing system and method |
7127856, | Jun 06 2003 | HAGEN, HANS T , JR ; HAGEN, HANS T , III | Insulated stud panel and method of making such |
7168216, | Jun 06 2003 | HAGEN, HANS T , JR ; HAGEN, HANS T , III; HAGEN JR , HANS T ; HAGEN, III, HANS T | Insulated stud panel and method of making such |
7574837, | Jun 06 2003 | HAGEN, JR HANS T ; HAGEN III , HANS T | Insulated stud panel and method of making such |
7905428, | Nov 24 2004 | PROBASCO, MAX A , MR | Multiple chemical sprayer |
8495852, | Nov 01 2011 | Johns, Manville | Methods and systems for insulating a building |
8789338, | Oct 03 2011 | Johns Manville | Methods and systems for sealing a wall |
8950142, | Nov 01 2011 | Johns Manville | Methods and systems for insulating a building |
9174362, | Jul 12 2011 | Castagra Products, Inc. | Solvent-free plural component spraying system and method |
9309663, | Nov 01 2011 | Johns Manville | Methods and systems for insulating a building |
9359758, | Oct 03 2011 | Johns Manville | Methods and systems for sealing a wall |
Patent | Priority | Assignee | Title |
4967956, | Jul 14 1986 | Glas-Craft, Inc.; GLAS-CRAFT, INC , A CORP OF IN | Multi-component spraying system |
5069881, | Jul 10 1990 | Mobay Corporation | Device and method for applying adhesives |
5178326, | Jul 14 1986 | Glas-Craft, Inc. | Industrial spraying system |
5379939, | Oct 15 1992 | FLEET CAPITAL CORPORATION,AS ADMINISTRATIVE AGENT | Single piece spray tip |
5405083, | Sep 20 1993 | AMERICAN MATRIX TECHNOLOGIES, INC | Spray gun with disposable mixer |
5820025, | Mar 20 1997 | HYDE TOOLS, INC | Reversible spray tip holder |
6062492, | May 15 1998 | Nordson Corporation | Viscous material dispense system |
6394644, | Jun 21 1999 | Sulzer Chemtech AG | Stacked static mixing elements |
6488991, | Dec 18 2001 | Nordson Corporation | Process for spraying one-component compositions with air-assisted, low pressure equipment having an improved spray nozzle |
DE19645614, | |||
DE29623922, |
Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
Apr 20 2001 | Bayer Polymers LLC | (assignment on the face of the patent) | / | |||
Apr 20 2001 | HUNTER, JACK H | Bayer Corporation | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 011740 | /0985 | |
Dec 26 2002 | Bayer Corporation | Bayer Polymers LLC | MASTER ASSIGNMENT OF PATENTS AGREEMENT AND ADDENDUM | 014035 | /0762 | |
Apr 22 2004 | Bayer Polymers LLC | Bayer MaterialScience LLC | CHANGE OF NAME SEE DOCUMENT FOR DETAILS | 023861 | /0905 | |
Feb 10 2010 | Bayer MaterialScience LLC | PLAS-PAK INDUSTRIES, INC | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 024045 | /0296 | |
Feb 14 2017 | PLAS-PAK INDUSTRIES, INC | Nordson Corporation | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 041256 | /0317 |
Date | Maintenance Fee Events |
Aug 24 2007 | M1551: Payment of Maintenance Fee, 4th Year, Large Entity. |
Apr 20 2011 | LTOS: Pat Holder Claims Small Entity Status. |
Jul 27 2011 | M2552: Payment of Maintenance Fee, 8th Yr, Small Entity. |
Aug 12 2015 | M2553: Payment of Maintenance Fee, 12th Yr, Small Entity. |
Date | Maintenance Schedule |
Feb 24 2007 | 4 years fee payment window open |
Aug 24 2007 | 6 months grace period start (w surcharge) |
Feb 24 2008 | patent expiry (for year 4) |
Feb 24 2010 | 2 years to revive unintentionally abandoned end. (for year 4) |
Feb 24 2011 | 8 years fee payment window open |
Aug 24 2011 | 6 months grace period start (w surcharge) |
Feb 24 2012 | patent expiry (for year 8) |
Feb 24 2014 | 2 years to revive unintentionally abandoned end. (for year 8) |
Feb 24 2015 | 12 years fee payment window open |
Aug 24 2015 | 6 months grace period start (w surcharge) |
Feb 24 2016 | patent expiry (for year 12) |
Feb 24 2018 | 2 years to revive unintentionally abandoned end. (for year 12) |